JPH04163385A - Method for treating waste laminated paper - Google Patents
Method for treating waste laminated paperInfo
- Publication number
- JPH04163385A JPH04163385A JP2288292A JP28829290A JPH04163385A JP H04163385 A JPH04163385 A JP H04163385A JP 2288292 A JP2288292 A JP 2288292A JP 28829290 A JP28829290 A JP 28829290A JP H04163385 A JPH04163385 A JP H04163385A
- Authority
- JP
- Japan
- Prior art keywords
- paper
- alkali
- waste
- laminated
- flakes
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000002699 waste material Substances 0.000 title abstract 3
- 238000000034 method Methods 0.000 title description 12
- 239000003513 alkali Substances 0.000 claims abstract description 13
- 239000010893 paper waste Substances 0.000 claims abstract description 12
- 230000032683 aging Effects 0.000 claims abstract description 7
- 239000002002 slurry Substances 0.000 claims abstract description 6
- 238000007865 diluting Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 238000003672 processing method Methods 0.000 claims description 2
- 239000000835 fiber Substances 0.000 abstract description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 5
- 239000008267 milk Substances 0.000 abstract description 3
- 210000004080 milk Anatomy 0.000 abstract description 3
- 235000013336 milk Nutrition 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000002994 raw material Substances 0.000 description 17
- 239000005001 laminate film Substances 0.000 description 13
- 238000012216 screening Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
Landscapes
- Paper (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、各種プラスチックフィルムや金属箔を積層し
たラミネート故紙、例えはミルクカートン等を処理し、
製紙用の良質繊維とするラミネート故紙処理方法に関す
るものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention is a method for processing laminated waste paper laminated with various plastic films or metal foils, such as milk cartons, etc.
The present invention relates to a method for processing laminated waste paper to produce high-quality fiber for paper manufacturing.
従来、ラミネート故紙(以下単に原料という)を処理し
て製紙用の良質繊維とするためには、パルパー内で原料
に温水及びNaOH等のアルカリを加え、スラリー濃度
4〜6%程度の低濃度においてポリエチレンフィルム等
のラミネートフィルムを離解して排棄し、製紙用の良質
繊維を得ることか行われている。Conventionally, in order to process laminated waste paper (hereinafter simply referred to as raw material) into high-quality fiber for paper manufacturing, warm water and alkali such as NaOH are added to the raw material in a pulper, and the slurry is mixed at a low concentration of about 4 to 6%. Laminated films such as polyethylene films are disintegrated and discarded to obtain high-quality fibers for paper manufacturing.
そして、この場合のパルパーとしては、第3図(A)に
示すように、タブ21内の底部付近に原料に回流を与え
るロータ22を回転可能に備え、このロータ22に近接
して5〜20mmφ程度の孔径をもつストレーナ23を
設け、ストレーナ23の下部を処理原料室24とし、処
理原料室24に排出管25を連結し、またタブ21内の
下方部に開閉バルブ26を備えたラミネートフィルム排
棄口27か設けられている。As shown in FIG. 3(A), the pulper in this case is rotatably equipped with a rotor 22 near the bottom of the tub 21 that gives circulation to the raw material, and a rotor 22 with a diameter of 5 to 20 mm in diameter is provided adjacent to the rotor 22. A strainer 23 with a hole diameter of about 100 mL is provided, the lower part of the strainer 23 is used as a processing raw material chamber 24, a discharge pipe 25 is connected to the processing raw material chamber 24, and a laminate film discharger is provided with an on-off valve 26 in the lower part of the tub 21. There are 27 exit ports.
ところで、このようなパルパーでは、第3図(B)に示
すように、原料を投入し、タブ21内に水張りし、アル
カリ添加後ロータ22を回転させて一定時間ラミネート
フィルムと繊維の離解を行い、その後処理原料を111
”出するという工程を数回繰り返したのち、タブ21内
を希釈し離解されてタブ内に溜まっているラミネートフ
ィルムを排棄していた。By the way, in such a pulper, as shown in FIG. 3(B), raw materials are introduced, the tub 21 is filled with water, and after adding alkali, the rotor 22 is rotated to disintegrate the laminate film and fibers for a certain period of time. , then the processed raw material is 111
``After repeating this process several times, the inside of the tub 21 was diluted and disintegrated, and the laminated film accumulated inside the tub was discarded.
このように、従来ては、パルパー内で離解されたラミネ
ートフィルムのタブ内滞留時間か長く、ラミネートフィ
ルムはロータ22の回転により破砕されて細片化され、
ストレーナ23を通過して処理原料室24内に至り、処
理原料と共に排出管25から排出されてしまう。処理原
料中の細片化されたラミホー1〜フイルムは、製品の品
質低下や抄紙機の操業性の低下につながるため、異物除
去工程に導いて除去しなくてはならないが、除去しにく
いた°めに第3図(A)に示すように処理原料を一旦チ
ェスト28に収容したのち粗選スクリーン29、精選ス
クリーン30などでの多段スクリーニング操作を余儀な
くされていた。As described above, conventionally, the residence time of the laminate film disintegrated in the pulper in the tub is long, and the laminate film is crushed into pieces by the rotation of the rotor 22.
It passes through the strainer 23, reaches the processing material chamber 24, and is discharged from the discharge pipe 25 together with the processing material. The shredded Lamiho film in the raw material to be processed leads to a decline in product quality and paper machine operability, so it must be removed by leading it to the foreign matter removal process, but it is difficult to remove. For this purpose, as shown in FIG. 3(A), after the raw material to be treated is once stored in a chest 28, a multi-stage screening operation using a rough screening screen 29, a fine screening screen 30, etc. is required.
しかしながら、ラミネートフィルムは原料中に多量に含
まれており、パルパー内ての原料離解処理中においてラ
ミネートフィルムは益々細片化され、しかも従来のパル
パーは前述したようにバッチ式操業であって連続運転が
できず、生産能率の悪いものであった。However, a large amount of laminate film is contained in the raw material, and during the raw material disintegration process in the pulper, the laminate film is increasingly broken into pieces. Moreover, as mentioned above, conventional pulpers operate in batch mode and do not operate continuously. This resulted in poor production efficiency.
本発明は、上記従来の問題点を解決し、ラミネートフィ
ルムと繊維の剥離を容易にし、ラミホー1〜フイルムの
細分化をできるたけ阻止し、後続するスクリーニング工
程を簡素化し、さらに連続運転を可能にして生産能率を
向上させることができるラミネート故紙処理方法を提供
することを目的とするものである。The present invention solves the above-mentioned conventional problems, facilitates the separation of the laminated film and fibers, prevents the lamination film from being fragmented as much as possible, simplifies the subsequent screening process, and enables continuous operation. The object of the present invention is to provide a method for processing laminated waste paper that can improve production efficiency.
本発明は、ラミネート故紙にアルカリを添加して大きな
フレーク状に離解したのち、タワー内で30分間以上熟
成し、次いでスラリー濃度10%以下に希釈して異物を
分離除去することを特徴とするラミネート故紙処理方法
である。The present invention is a laminate characterized by adding an alkali to laminated waste paper to disintegrate it into large flakes, aging it in a tower for 30 minutes or more, and then diluting the slurry to a concentration of 10% or less to separate and remove foreign substances. This is a waste paper processing method.
本発明の作用を、その一実施態様を示す図面を参照して
以下に説明する。The operation of the present invention will be explained below with reference to the drawings showing one embodiment thereof.
第1図において、ミルクカートン等の原料を離解装置1
内に投入し、NaOHなとのアルカリを添加し、場合に
より50°C程度の温水を供給し、スラリー濃度30%
以上、好ましくは濃度35〜40%において大きなフレ
ーク状に離解し排臭する。In Figure 1, raw materials such as milk cartons are disintegrated by a disintegrating device 1.
Add an alkali such as NaOH, and if necessary, supply hot water at about 50°C to make a slurry with a concentration of 30%.
As mentioned above, preferably at a concentration of 35 to 40%, it is disintegrated into large flakes and odor is removed.
離解装置1としては、例えば、上端部に入口、下端部に
出口を備え、傾斜してモータAにより回転するドラム2
内に、同軸でモータBによりドラム2の回転方向と反対
に回転する離解用突出片3をもつ回転軸4を配備し、濃
度30%以上の高濃度で離解することかできる、実公昭
49−24374号公報に示される型式のものか好まし
い。The disintegrating device 1 includes, for example, a drum 2 that has an inlet at the upper end and an outlet at the lower end, and is tilted and rotated by a motor A.
A rotary shaft 4 having a disintegrating protrusion 3 coaxially rotated by a motor B in the opposite direction to the rotational direction of the drum 2 is disposed inside, and the disintegration can be performed at a high concentration of 30% or more. The type shown in Japanese Patent No. 24374 is preferred.
この離解工程ては、はぼドライの原料に直接アルカリを
添加するから、少ない添加量でアルカリの吸収かよく、
ラミネートフィルムは剥離されやすくなり、粗大ラミネ
ートフィルムを短時間で剥離することかできる。In this disaggregation process, alkali is added directly to the raw material of Habo-dry, so a small amount of alkali is added and the alkali is absorbed well.
The laminate film is easily peeled off, and coarse laminate films can be peeled off in a short time.
このようにして離解装置lで粗大ラミネートフィルムが
除去された原料を、コンベア5によって底部に攪拌用イ
ンペラー6か配備された熟成塔7内に移送し、攪拌しな
がら熟成する。熟成時間は、少なくとも30分間とし、
それ以上に長ければ長い程よいか、30分〜24時間程
度とし、残留するラミネートフィルムと繊維を極めて容
易に離解しやすくする。The raw material from which the coarse laminate film has been removed in the disintegrating device 1 is transferred by a conveyor 5 into a ripening tower 7 equipped with a stirring impeller 6 at the bottom, where it is aged while being stirred. The aging time should be at least 30 minutes,
The longer the time, the better, or about 30 minutes to 24 hours, so that the remaining laminate film and fibers can be easily disintegrated.
熟成塔7て熟成された原料は、希釈水によって濃度を1
0%以下、好ましくは3%程度にまで希釈して、異物分
離機8に移送する。異物分離機8としては、ハイドロフ
ォイル付きの回転ドラムスクリーン、あるいは6〜8m
mφの丸孔を穿設した円形ストレーナ及びこのストレー
ナの目詰り防止のためのハイドロフォイル的形状をした
回転インペラーを備え、破砕作用の極めて少ないものを
使用し、ここで残留する異物を細片化することなく繊維
と離解し、かっ粗選を終了することができる。The raw material aged in the aging tower 7 is reduced in concentration to 1 with dilution water.
It is diluted to 0% or less, preferably about 3%, and transferred to the foreign matter separator 8. The foreign material separator 8 can be a rotating drum screen with hydrofoil or a 6 to 8 m
Equipped with a circular strainer with mφ round holes and a rotating impeller shaped like a hydrofoil to prevent clogging of this strainer, a strainer with extremely low crushing action is used to break the remaining foreign matter into small pieces. It is possible to disaggregate the fibers and complete the rough sorting without having to do anything.
従って、チエスト9に送られる原料は、離解及び粗選か
終了しており、そのまま精選スクリーン1゜に送って精
選し、製紙用の良質繊維を得ることができる。Therefore, the raw material sent to the CHEST 9 has already undergone disintegration and rough selection, and can be directly sent to the selection screen 1° for selection to obtain high-quality fibers for paper manufacturing.
以上述へたように、本発明は、ラミネート故紙にアルカ
リを添加して大きなフレーク状に離解したのち、タワー
内で30分間以上熟成し、次いでスラリー濃度10%以
下に希釈して異物を分離除去するもので、アルカリの使
用量少なく、容易にラミネートフィルムと繊維を分離す
ることかでき、しかもラミネートフィルムの細片化を防
止してスクリーニンク工程を簡素化し、さらに連続運転
を可能にして生産能率を向上させることかできる等の極
めて有益なる効果を存するものである。As mentioned above, the present invention involves adding alkali to laminated waste paper to disintegrate it into large flakes, aging it in a tower for 30 minutes or more, and then diluting the slurry to a concentration of 10% or less to separate and remove foreign substances. This reduces the amount of alkali used, makes it easy to separate the laminate film and fibers, and simplifies the screening process by preventing the laminate film from breaking into pieces. Furthermore, continuous operation is possible, increasing production efficiency. It has extremely beneficial effects, such as being able to improve
第1図は本発明の一実施態様を示すフローシート、第2
図は本発明で使用される装置の一例の構造図、第3図(
八)は従来の処理系統図、第3図(B)は第3図(A)
中の主要工程のフローシートである。
l 離解装置、2−・・1くラム、3・離解用突出片、
4・回転軸、5・・・コンベア、6 攪拌用インペラー
、7・熟成基、8・・・異物分離機、9 チェス1〜.
10 ・精選スクリーン、21 タブ、22 ロータ、
23 ストレーナ、24 処理原料室、25・排出管、
2G・・開閉バルブ、27・・・ラミネートフィルム排
臭口、28 チエスト、29・・・粗選スクリーン、3
0・・精選スクリーン。FIG. 1 is a flow sheet showing one embodiment of the present invention;
The figure is a structural diagram of an example of the device used in the present invention, and Figure 3 (
8) is a conventional processing system diagram, and Figure 3 (B) is Figure 3 (A).
This is a flow sheet of the main processes inside. l Disintegration device, 2-...1 ram, 3. Projection piece for disintegration,
4. Rotating shaft, 5... Conveyor, 6. Stirring impeller, 7. Aging group, 8.. Foreign matter separator, 9. Chess 1~.
10 ・Selection screen, 21 tab, 22 rotor,
23 strainer, 24 processing raw material chamber, 25/discharge pipe,
2G... Opening/closing valve, 27... Laminate film deodorizing port, 28 Chiest, 29... Rough selection screen, 3
0... Carefully selected screen.
Claims (1)
ーク状に離解したのち、タワー内で30分間以上熟成し
、次いでスラリー濃度10%以下に希釈して異物を分離
除去することを特徴とするラミネート故紙処理方法。(1) A laminated waste paper characterized by adding alkali to the laminated waste paper and disintegrating it into large flakes, aging it in a tower for 30 minutes or more, and then diluting the slurry to a concentration of 10% or less to separate and remove foreign substances. Processing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2288292A JPH04163385A (en) | 1990-10-29 | 1990-10-29 | Method for treating waste laminated paper |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2288292A JPH04163385A (en) | 1990-10-29 | 1990-10-29 | Method for treating waste laminated paper |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04163385A true JPH04163385A (en) | 1992-06-08 |
Family
ID=17728270
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2288292A Pending JPH04163385A (en) | 1990-10-29 | 1990-10-29 | Method for treating waste laminated paper |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04163385A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015078469A (en) * | 2013-10-18 | 2015-04-23 | 北越紀州製紙株式会社 | Regeneration method of waste paper containing waste laminate paper |
-
1990
- 1990-10-29 JP JP2288292A patent/JPH04163385A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2015078469A (en) * | 2013-10-18 | 2015-04-23 | 北越紀州製紙株式会社 | Regeneration method of waste paper containing waste laminate paper |
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